EP0633961A1 - Method and device for treating pulp. - Google Patents
Method and device for treating pulp.Info
- Publication number
- EP0633961A1 EP0633961A1 EP93908196A EP93908196A EP0633961A1 EP 0633961 A1 EP0633961 A1 EP 0633961A1 EP 93908196 A EP93908196 A EP 93908196A EP 93908196 A EP93908196 A EP 93908196A EP 0633961 A1 EP0633961 A1 EP 0633961A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fluid
- space
- suspension
- channel system
- permeable
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/02—Washing ; Displacing cooking or pulp-treating liquors contained in the pulp by fluids, e.g. wash water or other pulp-treating agents
Definitions
- the following invention relates to a method and a device for treating fibre suspensions, in particular for washing a fibre suspension in the form of cellulose pulp.
- fibre suspensions exhibit very special properties which demand special measures in connection with treating such suspensions. Washing a fibre suspension is an example of a treatment of this nature which requires special measures because of the special behaviour of a fibre suspension. More or less complicated apparatus for this purpose is already known.
- a feature possessed in common by these known processes and devices is, however, that, in connection with the actual liquid penetration phase, there is physical con ⁇ tact between a significant part of the fibre suspension and some form of sieving device. In connection with pulp production, in particular, such physical contact is undesirable since it gives rise to friction between the pulp bed and the sieving device, which in turn can cause disturbances in the feed-through of the pulp bed.
- An object of the present invention is to present a method and a device which make it possible to change the liquid content of a fibre suspension in an effective manner without exposing the pulp bed to undesirable physical stresses.
- Figure 1 shows a preferred embodiment of a device according to the invention
- Figure 2 shows an alternative embodiment of a device according to the invention.
- the device consists of an axle 1 which extends along a line of symmetry C.
- the axle 1 is arranged to be rotatable in a support 10 with the aid of bearing 7 and to be driven with the aid of a drive 8 in the form of a V-belt system.
- An arrangement 2, which is Y-shaped in longitudinal section, is connected to the axle 1 so that it turns with it.
- This Y-shaped arrangement 2 consists of a circular part 2A, 2B, which is liquid-permeable and which extends in an axial direction, a connecting part 2C, which extends essentially radially, and an inner base part 2D which at its inner periphery is connected to the said axle 1, in the preferred case by means of splines.
- the liquid-permeable part 2A, 2B possesses suitable perforations, for example in the form of circular holes or slits.
- a space 3 encloses the circular part 2A, 2B, which space will hereinafter be termed the fluid space 3.
- the " fluid space 3 is delimited outwards by a housing wall 4 which is essentially Y-shaped and which is suspended in bearing 7 by means of its base part 4B.
- a conical housing part 4C extends between the outermost cylindrical part 4A of the latter housing 4 and the base part 4B.
- the fluid space 3 communicates via a channel 5 with an inlet arrangement 6 for supplying a fluid, for example washing liquid.
- the channel 5 is delimited in its essential parts by a cover 17 which is firmly connected to the latter housing 4 by means of a flange 18.
- Suitable sealing elements 19 are arranged at those places where a rotating part meets a fixed part, such as, for example, at the connecting point between the said cover 17 and inlet arrangement 6.
- the inlet arrangement 9 for the pulp suspension is, in this preferred case, a cavity inside the axle 1 which opens out into a channel system 11 which extends essentially radially and which leads to the space 12 in which the change in the liquid content of the pulp suspension is to take place, which space will hereinafter be termed the displacement space 12.
- a channel system 15 is arranged centrally inside the device with an opening 15A, which is located relatively near to the narrowest part of the cone 4C.
- the opening 15A is arranged in a long pipe 15B which is fixed in a plate-like arrangement 20.
- the plate-like arrangement 20 also functions as a cover for the inlet arrangement 9 for the suspension and additionally constitutes one of the limiting surfaces for the channel 11 which leads to the displacement space 12.
- the plate 20 possesses a ring-shaped element 20A at its periphery, which element extends in an axial direction.
- a smaller pipe 15C leads from the larger pipe 15 to an outlet element 16 for fluid washing liquid or the like.
- Fibre suspension for example a pulp suspension which has passed through a bleaching step
- Fibre suspension is fed into the inlet arrangement 9, i.e. into the cavity in axle 1 of the device.
- the axle, and the parts 2, 4, 15 and 20 connected to the axle, are rotated at a relatively high rotation speed by means of the drive 8.
- the reason for the high rotation speed is the desire to establish relatively rapid layering between the fibre and liquid in the suspension as a result of the centrifugal force evoked by the rotation.
- the suspension will flow out of the open ⁇ ings in the axle and enter the channel 11 which leads to the displacement space 12.
- the suspension In this channel the suspension is subjected to a very rapid increase in speed, as a result of the rotation, and at the end of the channel swings in an axial direction and subsequently follows along the inner surface 2B of the liquid-permeable cylindrical part of the Y-shaped device 2, which is rotating in unison.
- the suspension will thereby be layered so that the heavier fibres come to lie in an outer layer and the lighter liquid in an inner layer.
- a liquid is supplied to the fluid space 3 at a static pressure which balances the pressure with which the fibre layer is acting in the direction of the inner wall 2B as a result of the centri ⁇ fugal force.
- both the layers will, due to the rotation and the conicity, move to the right in the diagram down to the narrowest part of the cone. In this region, a separation occurs in that a majority of the liquid is drawn off by turning away into pipe 15, while the fibre suspension will flow out through the centrally arranged outlet arrangement 14 to the right of the diagram.
- the liquid content of the outflowing fibre suspension can be regulated to a certain extent, i.e. with a large degree of negative pressure the percentage removal from the suspension is greater than with a low degree of negative pressure. It will be evident to the person skilled in the art that there are also many other factors which can be varied, thereby influencing the result. For example, increased rotational velocity requires increased counterpressure and also provides the possibility of higher through-flow since more rapid layering is achieved at higher rotational velocity etc.
- FIG. 2 shows an alternative embodiment of a device according to the invention, in which corresponding arrangements have been given the same reference numbers.
- the pulp and the washing liquid flow in in the same manner in this device as in that described above.
- the washing water (the constricted liquid) flows out centrally through its outlet arrangement 16 and the pulp suspension through an outlet arrangement 14 which is not centrally located.
- a long cylindrical part 21 has been built onto the plate arrangement 20 at the inlet channel 11, which cylindrical part, like the enclosing housing part 2A, 2B, is liquid-permeable. Through this cylindrical housing part 21, excess washing liquid is allowed to penetrate in towards the centre of the device.
- the housing wall is suspended at its other end on a further plate arrangement 22 which also forms a delimiting surface for the channel 13 which conducts the suspension out towards the outlet arrangement 14.
- the basic principle by which the two embodiments function is essentially the same. It will be evident to the person skilled in the art that the invention is not limited by that which has been demonstrated above but can be varied within the scope of the subsequent patent claims. Thus, it is, for example, also possible in an embodiment according to the second alternative to allow at least some of the liquid- permeable housing parts 2 and 21 to be conical to some degree. Other changes are to allow only certain parts of, for example, the outer liquid-permeable housing 2A, 2B to be liquid-permeable, for example to guarantee a definite layering before the pulp bed is subjected to counterpressure.
Landscapes
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Paper (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Fiber Materials (AREA)
- Absorbent Articles And Supports Therefor (AREA)
- Investigating Or Analysing Biological Materials (AREA)
- Combined Devices Of Dampers And Springs (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
- Preliminary Treatment Of Fibers (AREA)
- Ropes Or Cables (AREA)
- Fish Paste Products (AREA)
- Biological Treatment Of Waste Water (AREA)
- External Artificial Organs (AREA)
- Centrifugal Separators (AREA)
- Fluid-Damping Devices (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9201114A SE469232C (en) | 1992-04-08 | 1992-04-08 | Method and apparatus for washing cellulose pulp |
SE9201114 | 1992-04-08 | ||
PCT/SE1993/000115 WO1993021377A1 (en) | 1992-04-08 | 1993-02-16 | Method and device for treating pulp |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0633961A1 true EP0633961A1 (en) | 1995-01-18 |
EP0633961B1 EP0633961B1 (en) | 1996-05-22 |
Family
ID=20385893
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP93908196A Expired - Lifetime EP0633961B1 (en) | 1992-04-08 | 1993-02-16 | Method and device for treating pulp |
Country Status (13)
Country | Link |
---|---|
US (1) | US5556508A (en) |
EP (1) | EP0633961B1 (en) |
JP (1) | JPH07505684A (en) |
AT (1) | ATE138432T1 (en) |
AU (1) | AU665080B2 (en) |
BR (1) | BR9306212A (en) |
CA (1) | CA2132202C (en) |
DE (1) | DE69302811D1 (en) |
FI (1) | FI116072B (en) |
NO (1) | NO943769L (en) |
RU (1) | RU94046046A (en) |
SE (1) | SE469232C (en) |
WO (1) | WO1993021377A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE503504C2 (en) * | 1994-10-20 | 1996-06-24 | Kvaerner Pulping Tech | Apparatus for treating fiber suspension |
SE517532C2 (en) * | 2000-10-25 | 2002-06-18 | Rolf Ekholm | Method and apparatus for washing a fiber suspension |
CN103923218B (en) * | 2014-04-21 | 2016-03-30 | 铜仁学院 | A kind of nano micro crystal cellulose cleaning and spin-drying device |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE113137C1 (en) * | ||||
GB2059469B (en) * | 1979-09-26 | 1983-09-01 | Reed International Ltd | Washing fibre stock |
FI79867C (en) * | 1988-04-13 | 1990-03-12 | Ahlstroem Oy | FOERFARANDE OCH ANORDNING FOER BEHANDLING AV FIBERSUSPENSIONER. |
US5013460A (en) * | 1989-11-13 | 1991-05-07 | Kamyr, Inc. | Centrifugal washer for paper pulp with means to feed pulp as a thin sheet |
FI900273A (en) * | 1990-01-17 | 1991-07-18 | Tampella Oy Ab | ANORDINATION FOR THE FIBER OF THE FIBER. |
US5204009A (en) * | 1991-08-14 | 1993-04-20 | Kvaerner Hymac Inc. | Slurry rising apparatus and method therefor |
-
1992
- 1992-04-08 SE SE9201114A patent/SE469232C/en not_active IP Right Cessation
-
1993
- 1993-02-16 DE DE69302811T patent/DE69302811D1/en not_active Expired - Lifetime
- 1993-02-16 US US08/313,135 patent/US5556508A/en not_active Expired - Lifetime
- 1993-02-16 JP JP5518215A patent/JPH07505684A/en active Pending
- 1993-02-16 CA CA002132202A patent/CA2132202C/en not_active Expired - Fee Related
- 1993-02-16 RU RU94046046/12A patent/RU94046046A/en unknown
- 1993-02-16 EP EP93908196A patent/EP0633961B1/en not_active Expired - Lifetime
- 1993-02-16 AT AT93908196T patent/ATE138432T1/en not_active IP Right Cessation
- 1993-02-16 AU AU39460/93A patent/AU665080B2/en not_active Ceased
- 1993-02-16 BR BR9306212A patent/BR9306212A/en not_active Application Discontinuation
- 1993-02-16 WO PCT/SE1993/000115 patent/WO1993021377A1/en active IP Right Grant
-
1994
- 1994-10-04 FI FI944620A patent/FI116072B/en active IP Right Grant
- 1994-10-06 NO NO943769A patent/NO943769L/en unknown
Non-Patent Citations (1)
Title |
---|
See references of WO9321377A1 * |
Also Published As
Publication number | Publication date |
---|---|
AU665080B2 (en) | 1995-12-14 |
EP0633961B1 (en) | 1996-05-22 |
SE9201114L (en) | 1993-06-07 |
SE9201114D0 (en) | 1992-04-08 |
SE469232B (en) | 1993-06-07 |
US5556508A (en) | 1996-09-17 |
JPH07505684A (en) | 1995-06-22 |
DE69302811D1 (en) | 1996-06-27 |
NO943769D0 (en) | 1994-10-06 |
RU94046046A (en) | 1996-07-27 |
FI116072B (en) | 2005-09-15 |
NO943769L (en) | 1994-10-06 |
FI944620A0 (en) | 1994-10-04 |
AU3946093A (en) | 1993-11-18 |
CA2132202C (en) | 2003-01-21 |
SE469232C (en) | 1997-04-29 |
FI944620A (en) | 1994-10-04 |
WO1993021377A1 (en) | 1993-10-28 |
ATE138432T1 (en) | 1996-06-15 |
BR9306212A (en) | 1998-06-23 |
CA2132202A1 (en) | 1993-10-28 |
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Legal Events
Date | Code | Title | Description |
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